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US3445244A - Solid vinegar - Google Patents

Solid vinegar Download PDF

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Publication number
US3445244A
US3445244A US527729A US3445244DA US3445244A US 3445244 A US3445244 A US 3445244A US 527729 A US527729 A US 527729A US 3445244D A US3445244D A US 3445244DA US 3445244 A US3445244 A US 3445244A
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United States
Prior art keywords
vinegar
dextrin
solids
spray dried
gum
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US527729A
Inventor
Peter Paul Noznick
Charles W Tatter
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beatrice Companies Inc
Original Assignee
Beatrice Foods Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
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Publication of US3445244A publication Critical patent/US3445244A/en
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Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12JVINEGAR; PREPARATION OR PURIFICATION THEREOF
    • C12J1/00Vinegar; Preparation or purification thereof

Definitions

  • the present invention relates to spray drying vinegar.
  • Another object is to entrap the characteristic vinegar flavor in a dry powder.
  • the preferred enrobing agent is gum arabic.
  • dextrin as a coating or en-robing agent.
  • carbohydrate gums such as gum tragacanth.
  • fats and/or emulsifiers e.g. mono and di glycerides to (1) absorb fat soluble flavors, (2) prevent dusting of the final powder and (3) to cut down foaming during processing.
  • Suitable fats include vegetable fats such as cocoanut oil, hydrogenated castor oil, hydrogenated cottonseed oil, corn oil, safllower oil, peanut oil.
  • the vinegar can be from 60 grain to 500 grain, with 200-400 grain vinegar (i.e. 20-40%) being preferred. It is not economically feasible to use vinegar below 60 grain because of the large amount of water which must be removed.
  • the spray dried vinegar products of the present invention can be used to impart vinegar flavor in dry form for salad dressings, sour cream, spaghetti sauce, dry mix preparations, etc.
  • the aqueous mixture which is spray dried has 25-60% solids (i.e. nonvvater) content. It is preferred to use as high a solids concentration as is possible so as to keep the drying rate at a maximum and the resultant powder at the lowest temperature.
  • the solids content prior to drying should be such as to give a fluid, homogenous emulsion.
  • Percent Vinegar 5 to 60 Gum acacia 25 to 95 United States Patent 0 Fee
  • dextrin When dextrin is employed it is used in an amount of 30 to of total solids.
  • Gelatin when employed, is used in an amount of 2 to 20%.
  • Fats when employed, are used in an amount of 0.1 to 10%.
  • Mono and di glycerides are used in the same amount as the fats.
  • the aqueous mixture of gum or dextrin is normally pasteurized, e.g. at 140-165 F.
  • the vinegar is not added to the hot gum or dextrin solution or volatile materials will be lost.
  • the temperature therefore is preferably lowered to not over 125 F., most preferably at IOU- F. prior to addition of the vinegar.
  • the emulsion should be well homogenized to entrap the vinegar flavor. Homogenization pressures are usually in the range of 1000-5000 p.s.i.
  • Example 1 Parts White vinegar solids 20 Gum acacia 80
  • the method of preparation was as follows: Gum acacia was dissolved in enough warm water to give a 35% total aqueous solids suspension after addition of the vinegar. (The term solids as used in the present specification when applied to vinegar includes all the nonaqueous portion of the vinegar.)
  • the gum acacia solution was pasteurized at 160 F. for 30 minutes, cooled to F. and concentrated (300 grain) white vinegar added. The batch was stirred until uniform, homogenized at 2000 psi. and spray dried in a horizontal concurrent flow spray dryer at 350 F.
  • a similar spray dried product was obtained by replacing the white vinegar by cider vinegar.
  • Example 2 Parts White vinegar solids 50 Gum acacia solids 50 The process of Example 1 was repeated to produce a spray dried vinegar enrobed in the gum acacia.
  • Example 3 Parts White vinegar solids 20 Gum acacia '65 Gelatin type A 15 The process of Example 1 was repeated to produce a spray dried vinegar product.
  • Example 4 Parts White vinegar solids 20 Globe yellow dextrin 80 The procedure of Example 1 was repeated to obtain spray dried vinegar enrobed in the dextrin.
  • Example 5 Parts White vinegar solids 50 Globe yellow dextrin 50 The procedure of Example 1 was repeated to obtain spray dried vinegar enrobed in the dextrin.
  • Example 6 Parts White vinegar solids 20 Globe yellow dextrin 65 Gelatin, type A 15 The procedure of Example 1 was repeated to obtain 3 spray dried vinegar enrobed in a mixture of dextrin and gelat'm.
  • a composition comprising to 60% spray dried vinegar enrobed in a spray dried member of the group consisting of 25 to 95% carbohydrate gums and 30 to 95% dextrin.
  • a product according to claim 1 including 2 to of a member of the group consisting of gelatin and gluten.
  • a product according to claim 1 containing 5 to 60% vinegar and to 95 gum acacia.
  • a product according to claim 3 including 2 to 20% of gelatin.
  • a product according to claim 1 containing 5 to 60% vinegar and to 95% dextrin.
  • a product according to claim 5 including 2 to 20% gelatin.
  • a process of preparing the product of claim 1 comprising passing an aqueous mixture containing 25 to solids of vinegar and an enrobing agent of the group consisting of carbohydrate gums and dextrin wherein the solids comprise 5-60% vinegar and 25-95% of the References Cited UNITED STATES PATENTS 4/1931 Bornegg 99-206 9/ 1960 Sanna -9956 FOREIGN PATENTS 23,064 10/ 1963 Japan.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Food Science & Technology (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Seasonings (AREA)
  • Jellies, Jams, And Syrups (AREA)

Description

3,445,244 SOLID VINEGAR Peter Paul Noznick, Evanston, and Charles W. Tatter, Homewood, Ill., assignors to Beatrice Foods Co., Chicago, 11]., a corporation of Delaware No Drawing. Filed Feb. 16, 1966, Ser. No. 527,729
Int. Cl. C12j 1/00 US. Cl. 99-147 9 Claims ABSTRACT OF THE DISCLOSURE Aqueous vinegar is spray dried with a carbohydrate gum or dextrin as an enrobing agent. Gelatin or gluten can also be present.
The present invention relates to spray drying vinegar.
It is an object of the present invention to form spray dried vinegar.
Another object is to entrap the characteristic vinegar flavor in a dry powder.
Still further objects and the entire scope of applicability of the present invention will become apparent from the detailed description given hereinafter; it should be understood, however, that the detailed description and specific examples, while indicating preferred embodiments of the invention, are given by way of illustration only, since various changes and modifications within the spirit and scope of the invention will become apparent to those skilled in the art from this detailed description.
It has now been found that these objects can be attained by spray drying vinegar in the presence of an enrobing agent.
The preferred enrobing agent is gum arabic. In place of all or part of the gum arabic there can be used dextrin as a coating or en-robing agent. Also, there can be used other carbohydrate gums such as gum tragacanth.
There can also be used certain proteins in conjunction with the gum arabic and/or dextrin. Thus, there can be employed A type gelatin and gluten (the acid soluble protein from wheat).
Optionally, there can be added fats and/or emulsifiers, e.g. mono and di glycerides to (1) absorb fat soluble flavors, (2) prevent dusting of the final powder and (3) to cut down foaming during processing. Suitable fats include vegetable fats such as cocoanut oil, hydrogenated castor oil, hydrogenated cottonseed oil, corn oil, safllower oil, peanut oil.
The vinegar can be from 60 grain to 500 grain, with 200-400 grain vinegar (i.e. 20-40%) being preferred. It is not economically feasible to use vinegar below 60 grain because of the large amount of water which must be removed.
The spray dried vinegar products of the present invention can be used to impart vinegar flavor in dry form for salad dressings, sour cream, spaghetti sauce, dry mix preparations, etc.
Unless otherwise indicated, all parts and percentages are by weight.
Usually the aqueous mixture which is spray dried has 25-60% solids (i.e. nonvvater) content. It is preferred to use as high a solids concentration as is possible so as to keep the drying rate at a maximum and the resultant powder at the lowest temperature. The solids content prior to drying should be such as to give a fluid, homogenous emulsion.
The range of proportions of materials which can be employed are as follows:
Percent Vinegar (nonaqueous basis) 5 to 60 Gum acacia 25 to 95 United States Patent 0 Fee When dextrin is employed it is used in an amount of 30 to of total solids. Gelatin, when employed, is used in an amount of 2 to 20%. Fats, when employed, are used in an amount of 0.1 to 10%. Mono and di glycerides are used in the same amount as the fats.
The aqueous mixture of gum or dextrin is normally pasteurized, e.g. at 140-165 F.
Preferably, the vinegar is not added to the hot gum or dextrin solution or volatile materials will be lost. The temperature therefore is preferably lowered to not over 125 F., most preferably at IOU- F. prior to addition of the vinegar. The emulsion should be well homogenized to entrap the vinegar flavor. Homogenization pressures are usually in the range of 1000-5000 p.s.i.
When employing dextrin it is important to keep the contact time between the aqueous acid and dextrin at a minimum to prevent hydrolysis.
Example 1 Parts White vinegar solids 20 Gum acacia 80 In the above example the method of preparation was as follows: Gum acacia was dissolved in enough warm water to give a 35% total aqueous solids suspension after addition of the vinegar. (The term solids as used in the present specification when applied to vinegar includes all the nonaqueous portion of the vinegar.) The gum acacia solution was pasteurized at 160 F. for 30 minutes, cooled to F. and concentrated (300 grain) white vinegar added. The batch was stirred until uniform, homogenized at 2000 psi. and spray dried in a horizontal concurrent flow spray dryer at 350 F.
A similar spray dried product was obtained by replacing the white vinegar by cider vinegar.
Example 2 Parts White vinegar solids 50 Gum acacia solids 50 The process of Example 1 was repeated to produce a spray dried vinegar enrobed in the gum acacia.
Example 3 Parts White vinegar solids 20 Gum acacia '65 Gelatin type A 15 The process of Example 1 was repeated to produce a spray dried vinegar product.
Example 4 Parts White vinegar solids 20 Globe yellow dextrin 80 The procedure of Example 1 was repeated to obtain spray dried vinegar enrobed in the dextrin.
Example 5 Parts White vinegar solids 50 Globe yellow dextrin 50 The procedure of Example 1 was repeated to obtain spray dried vinegar enrobed in the dextrin.
Example 6 Parts White vinegar solids 20 Globe yellow dextrin 65 Gelatin, type A 15 The procedure of Example 1 was repeated to obtain 3 spray dried vinegar enrobed in a mixture of dextrin and gelat'm.
We claim:
1. A composition comprising to 60% spray dried vinegar enrobed in a spray dried member of the group consisting of 25 to 95% carbohydrate gums and 30 to 95% dextrin.
2. A product according to claim 1 including 2 to of a member of the group consisting of gelatin and gluten.
3. A product according to claim 1 containing 5 to 60% vinegar and to 95 gum acacia.
4. A product according to claim 3 including 2 to 20% of gelatin.
5. A product according to claim 1 containing 5 to 60% vinegar and to 95% dextrin.
6. A product according to claim 5 including 2 to 20% gelatin.
7. A process of preparing the product of claim 1 comprising passing an aqueous mixture containing 25 to solids of vinegar and an enrobing agent of the group consisting of carbohydrate gums and dextrin wherein the solids comprise 5-60% vinegar and 25-95% of the References Cited UNITED STATES PATENTS 4/1931 Bornegg 99-206 9/ 1960 Sanna -9956 FOREIGN PATENTS 23,064 10/ 1963 Japan.
RAYMOND N. JONES, Primary Examiner.
R. B. ANDEWELT, Assistant Examiner.
US. Cl. X.R. 99-199
US527729A 1966-02-16 1966-02-16 Solid vinegar Expired - Lifetime US3445244A (en)

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US52772966A 1966-02-16 1966-02-16

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3630756A (en) * 1970-03-18 1971-12-28 Ross Alexander Smith Vinegar-type flavor composition
US3898344A (en) * 1973-05-24 1975-08-05 Us Army Packaged dry imitation vinegar product
US4713251A (en) * 1985-12-18 1987-12-15 Durkee Industrial Foods Corp. Process for encapsulating liquid acids and product
FR2755610A1 (en) * 1996-11-14 1998-05-15 Dukan Pierre Preparation of dry extract from vinegar that has been enriched with sludge from filtration of crude vinegar
US20120201950A1 (en) * 2005-09-15 2012-08-09 Triad Resource Technologies, Llc Compositions for improving flavor and safety of marinated meat products
US20120208740A1 (en) * 2011-02-14 2012-08-16 Chemlink Laboratories, Llc Method for preparing a solid form of acetic acid and products thereof
US20150225683A1 (en) * 2012-08-01 2015-08-13 Purac Biochem B.V. Preparation of a powdered vinegar

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1800501A (en) * 1924-03-11 1931-04-14 Fruit Growers Exchange Ca Method of drying fruit juices
US2953457A (en) * 1957-06-24 1960-09-20 Sanna Dairies Inc Method for drying food materials

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1800501A (en) * 1924-03-11 1931-04-14 Fruit Growers Exchange Ca Method of drying fruit juices
US2953457A (en) * 1957-06-24 1960-09-20 Sanna Dairies Inc Method for drying food materials

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3630756A (en) * 1970-03-18 1971-12-28 Ross Alexander Smith Vinegar-type flavor composition
US3898344A (en) * 1973-05-24 1975-08-05 Us Army Packaged dry imitation vinegar product
US4713251A (en) * 1985-12-18 1987-12-15 Durkee Industrial Foods Corp. Process for encapsulating liquid acids and product
FR2755610A1 (en) * 1996-11-14 1998-05-15 Dukan Pierre Preparation of dry extract from vinegar that has been enriched with sludge from filtration of crude vinegar
US9578893B2 (en) 2005-09-15 2017-02-28 Triad Resource Technologies, Llc Compositions for improving flavor and safety of marinated meat products
US8877280B2 (en) * 2005-09-15 2014-11-04 Triad Resource Technologies, Llc Compositions for improving flavor and safety of marinated meat products
US20120201950A1 (en) * 2005-09-15 2012-08-09 Triad Resource Technologies, Llc Compositions for improving flavor and safety of marinated meat products
US20120208740A1 (en) * 2011-02-14 2012-08-16 Chemlink Laboratories, Llc Method for preparing a solid form of acetic acid and products thereof
US8859482B2 (en) * 2011-02-14 2014-10-14 Chemlink Laboratories, Llc Method for preparing a solid form of acetic acid and products thereof
US9068146B2 (en) 2011-02-14 2015-06-30 Chemlink Laboratories, Llc Solid form of acetic acid and products thereof
US20150225683A1 (en) * 2012-08-01 2015-08-13 Purac Biochem B.V. Preparation of a powdered vinegar
EP2880146B1 (en) 2012-08-01 2016-10-26 Purac Biochem bv Preparation of a powdered vinegar
EP3115448A1 (en) * 2012-08-01 2017-01-11 Purac Biochem B.V. Preparation of a powdered vinegar
US10752871B2 (en) * 2012-08-01 2020-08-25 Purac Biochem B.V. Preparation of a powdered vinegar
US11466238B2 (en) 2012-08-01 2022-10-11 Purac Biochem B.V. Preparation of a powdered vinegar
US12252674B2 (en) 2012-08-01 2025-03-18 Purac Biochem B.V. Preparation of a powdered vinegar

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